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Catalyst for carbonylation of dimethyl ether, preparation method and application thereof

A technology of dimethyl ether and carbonylation, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, carbon monoxide or formate reaction preparation, etc., which can solve the problems of easy clogging of molecular sieves, unfavorable reaction activity of butene isomerization reaction, etc. question

Active Publication Date: 2020-05-08
ZHENGZHOU TOBACCO RES INST OF CNTC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] The Chinese invention patent with the publication number of CN 101475432A discloses a method for the selectivity of butene double bond isomerization reaction. The method of pre-carbon deposition is used to prepare a pre-carbon-deposited aluminosilicate catalyst to improve the isomerization of butene double bonds. However, the starting point of this patent is that the strong acid sites in the pores are covered by pre-carbon deposition, while the weak acid sites that play a role in isomerization are not covered, and the molecular sieves are easily blocked in the preparation method of pre-carbon deposition catalysts The orifice is unfavorable to the reactivity of the subsequent butene isomerization reaction

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  • Catalyst for carbonylation of dimethyl ether, preparation method and application thereof
  • Catalyst for carbonylation of dimethyl ether, preparation method and application thereof
  • Catalyst for carbonylation of dimethyl ether, preparation method and application thereof

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Embodiment 1

[0043] The preparation method of the catalyst of the dimethyl ether carbonylation of the present embodiment, such as figure 1 shown, including the following steps:

[0044] 1) Converting mordenite molecular sieves into hydrogen-type mordenite by ammonia exchange method, filling hydrogen-type mordenite in a fixed-bed reactor, and heating to 400° C. for 1 hour activation under nitrogen atmosphere;

[0045] 2) After activation, lower the temperature to 300° C. and feed propylene into the catalyst bed for catalytic reaction. When the conversion rate of propylene is lower than 5%, stop feeding the substrate, and use nitrogen to purge the catalyst bed to lower the temperature to obtain precursor A ;

[0046] 3) Precursor A was placed in a high-temperature furnace, and the temperature was raised to 900°C for 1 hour under nitrogen at a heating rate of 100°C / min to obtain precursor B;

[0047] 4) Mix the precursor B obtained in step 3) with the dispersant methanol, place it in a plan...

Embodiment 2

[0050] The preparation method of the catalyst of the dimethyl ether carbonylation of the present embodiment comprises the following steps:

[0051] 1) Converting mordenite molecular sieves into hydrogen-type mordenite by ammonia exchange method, filling hydrogen-type mordenite in a fluidized bed reactor, and heating to 400° C. for 1 hour activation under nitrogen atmosphere;

[0052]2) After activation, feed isobutene into the catalyst bed at 400°C for catalytic reaction. When the conversion rate of isobutene is lower than 5%, stop feeding the substrate, and use helium to blow the catalyst bed to lower the temperature to obtain precursor A ;

[0053] 3) Precursor A was placed in a high-temperature furnace, and the temperature was raised to 600°C for 4 hours under the protection of nitrogen at a heating rate of 100°C / min to obtain precursor B;

[0054] 4) Mix the precursor B obtained in step 3) with the dispersant methanol and water, place it in a planetary ball mill and mill ...

Embodiment 3

[0057] The preparation method of the catalyst of the dimethyl ether carbonylation of the present embodiment comprises the following steps:

[0058] 1) The mordenite molecular sieve is converted into hydrogen-type mordenite by ammonia exchange method, and the hydrogen-type mordenite is loaded in a moving bed reactor, and heated to 450° C. for 1 hour activation under nitrogen atmosphere;

[0059] 2) After activation, feed 1-pentene into the catalyst bed at 450°C for catalytic reaction. When the conversion rate of 1-pentene is lower than 5%, stop feeding the substrate, and use helium to sweep the catalyst bed Lower the temperature to obtain precursor A;

[0060] 3) Precursor A was placed in a high-temperature furnace, and the temperature was raised to 500°C for 8 hours at a heating rate of 100°C / min under nitrogen gas to obtain precursor B;

[0061] 4) Mix the precursor B obtained in step 3) with the dispersant methanol, place it in a planetary ball mill and mill it at a speed o...

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Abstract

The invention relates to a catalyst for carbonylation of dimethyl ether as well as a preparation method and an application of the catalyst and belongs to the technical field of catalytic chemistry. The preparation method of the catalyst for carbonylation of dimethyl ether comprises the following steps: 1) an activated hydrogen molecular sieve and small-molecular-weight organic matter react at 300-600 DEG C, and a precursor A is obtained, wherein the molecular dynamic diameter of the small-molecular-weight organic matter is 0.4-0.7 nm; 2) under inert gas protection, the precursor A obtained in the step 1) is heated to 500-900 DEG C and carbonized for 1-10 h, and a precursor B is obtained; 3) the precursor B and a dispersing agent are subjected to mixed ball milling, mixed slurry is obtained, then solid-liquid separation is performed, and a precursor C is obtained; 4) the precursor C is mixed with organic acid at 20-80 DEG C for 1-10 h, and the catalyst is obtained; the molecular dynamic diameter of the organic acid is not smaller than 0.50 nm. The catalyst prepared with the method and used for carbonylation of dimethyl ether has high selectivity and long service life in carbonylation of dimethyl ether.

Description

technical field [0001] The invention relates to a catalyst for carbonylation of dimethyl ether, a preparation method and application thereof, and belongs to the technical field of chemical catalysis. Background technique [0002] Methyl acetate (methyl acetate) is widely used in textile, perfume and pharmaceutical industries, and is an important intermediate of organic raw materials. The downstream products mainly include acetic acid, acetic anhydride, methyl acrylate, vinyl acetate, acetamide, etc. In China, the production of methyl acetate mainly utilizes the traditional esterification method. This method has the problems of complex separation of product and catalyst, expensive and scarce precious metal rhodium, and iodides cause severe corrosion to equipment. Solid acid catalyzed carbonylation of dimethyl ether to produce methyl acetate is a novel route. The catalyst used in the process is a solid catalyst, which is easy to separate without corrosion and can solve the pr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/18B01J37/08B01J37/00B01J37/06C07C67/37C07C69/14
CPCB01J29/18B01J37/00B01J37/06B01J37/084C07C67/37C07C69/14
Inventor 王金棒程多福高运谦邱纪青汪志波洪广峰张仕华刘亚丽郑路贾楠郑新章
Owner ZHENGZHOU TOBACCO RES INST OF CNTC